Compositions and methods for well cementing

ABSTRACT

The effectiveness of expansive cement systems may be diluted when, during a well cementing operation, commingling takes place between the cement slurry and a spacer fluid, a drilling fluid, or both. Incorporating expansive agents in the spacer fluid or drilling fluid may reduce or negate the loss of expansion at the cement slurry/spacer interface or the cement slurry/drilling fluid interface, thereby promoting zonal isolation throughout the cemented interval.

BACKGROUND

The statements in this section merely provide background informationrelated to the present disclosure and may not constitute prior art.

The present disclosure broadly relates to well cementing. Moreparticularly the invention relates to compositions that containmaterials that expand upon hydration, thereby improving zonal isolationin a subterranean well.

Good bonding between set cement and casing, and between the set cementand the formation, is essential for effective zonal isolation. Poorbonding limits production, and reduces the effectiveness of stimulationtreatments. Communication between zones can be caused by inadequatedrilling fluid removal, poor cement/formation bonding, expansion andcontraction of the casing resulting from internal pressure or thermalstress, and cement contamination by drilling or formation fluids. Undersuch circumstances, a small gap or “microannulus” may develop at thecement/casing or the cement/formation interface.

Cement systems that expand slightly after setting are a proven means ofsealing microannuli and improving primary cementing results. Theimproved bonding is the result of mechanical resistance or tightening ofthe cement against the pipe and formation. Portland cement manufacturerslimit the amount of certain alkaline impurities to avoid expansion ofthe set cement, a condition called “unsoundness.” In an unrestrainedenvironment such as a road or building, expansion of the set cement canresult in cracking and failure. In a wellbore environment, however, thecement is restrained by the casing and, when competent, the formation;consequently, once the cement has expanded to eliminate void spaces,further expansion reduces internal cement porosity.

Most expansive well cement systems rely upon the formation of themineral ettringite, after the cement has set. Ettringite crystals have agreater bulk volume than the components from which they form;consequently, expansion occurs because of the internal pressure exertedupon crystallization. Today the most common method for preparingettringite-base expansive cements is to add calcium sulfate hemihydrate(CaSO₄·½ H₂O) to a portland cement that contains at least 5 wt %tricalcium aluminate (abbreviated as C₃A). A limitation ofettringite-base systems is their inability to provide significantexpansion at curing temperatures above about 170° F. (76° C.).Ettringite is not stable at higher temperatures, and converts to a moredense calcium sulfoaluminate hydrate and gypsum.

Cement slurries containing high concentrations of NaCl, Na₂SO₄ or bothwere among the earliest expansive well cements. After setting, cementexpansion occurs because of internal pressure exerted by thecrystallization of the salts within pores, and by chlorosilicatereactions. These systems are effective at temperatures up to about 400°F. (204° C.).

Calcium oxide and magnesium oxide provide an expansive force within thecement matrix resulting from hydration to their respective hydroxides.The hydrated material occupies more space than that of the originalingredients. CaO may be more effective than MgO at curing temperaturesbelow about 60° C. (140° F.). For well cementing operations, MgO may becalcined at temperatures between about 700° C. and 2000° C., or between1100° C. and 1300° C. Such calcination may delay the expansion reactionuntil after the cement slurry sets. In some cases, blends of CaO andcalcined MgO may be employed to provide effective expansion throughout awider curing temperature range.

A thorough discussion concerning expanding cement systems may be foundin the following publication. Nelson E B et al.: “Special CementSystems,” in Nelson E B and Guillot D (eds.): Well Cementing—2^(nd)Edition, Schlumberger (2006) 235-237.

During a well cementing operation, the cement slurry may contact aspacer fluid or a drilling fluid. During displacement in the well,operators endeavor to minimize commingling of the cement slurry withother fluids; however, should such commingling take place, dilution ofthe cement slurry may occur, possibly resulting in suboptimal zonalisolation.

SUMMARY

Applicant has determined that including one or more expanding agents ina spacer fluid, drilling fluid or both may minimize the deleteriouseffects arising from commingling with the cement slurry, therebypreserving cement slurry expansion and promoting zonal isolation.

In an aspect, embodiments relate to compositions comprising water, aviscosifying agent and an expanding agent comprising calcium oxide orcalcined magnesium oxide or both.

In a further aspect, embodiments relate to methods comprising preparinga spacer fluid the comprises water, a viscosifying agent and anexpanding agent comprising calcium oxide, calcined magnesium oxide orboth. During a well cementing operation, the spacer fluid is placed inthe well such that the spacer fluid flows between a drilling fluid and acement slurry. The spacer fluid commingles with the drilling fluid orthe cement slurry, thereby forming an interface. The cement slurry andthe interface are cured, wherein the interface expands or does notshrink upon the curing.

In a further aspect, embodiments relate to compositions comprising anon-aqueous liquid and an expanding agent comprising calcium oxide orcalcined magnesium oxide or both.

In a further aspect, embodiments relate to methods comprising preparinga drilling fluid comprising a non-aqueous fluid and an expanding agentcomprising calcium oxide or calcined magnesium oxide or both. During awell cementing operation, the drilling fluid is placed in the well suchthat the drilling fluid flows ahead of a cement slurry. The drillingfluid commingles with the cement slurry, thereby forming an interface.The cement slurry and the interface are cured, wherein the interfaceexpands or does not shrink upon the curing.

In a further aspect, embodiments relate to compositions comprising anaqueous cement slurry and a non-aqueous additive comprising a suspensionof an expanding agent comprising calcium oxide or a mixture of calciumoxide and calcined magnesium oxide.

In a further aspect, embodiments relate to methods comprising preparinga composition comprising an aqueous cement slurry and a non-aqueousadditive comprising a suspension of an expanding agent comprisingcalcium oxide and calcined magnesium oxide or both. During a wellcementing operation, the cement slurry is placed in the well such thatthe cement slurry flows behind a spacer fluid or a drilling fluid orboth. The spacer fluid or the drilling fluid may commingle with thecement slurry, thereby forming an interface. The cement slurry and theinterface are cured, wherein the interface expands or does not shrinkupon the curing.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a photograph of a linear expansion cell.

FIG. 2 presents linear expansion data from expansive cement slurriescontaminated by an oil-base drilling fluid, with and without anexpansion agent in the drilling fluid.

FIG. 3 presents linear expansion data from expansive cement slurriescontaminated by an aqueous spacer fluid, with and without an expansionagent in the spacer fluid.

DETAILED DESCRIPTION

In the following description, numerous details are set forth to providean understanding of the present disclosure. However, it may beunderstood by those skilled in the art that the methods of the presentdisclosure may be practiced without these details and that numerousvariations or modifications from the described embodiments may bepossible.

At the outset, it should be noted that in the development of any suchactual embodiment, numerous implementation—specific decisions are madeto achieve the developer's specific goals, such as compliance withsystem related and business related constraints, which will vary fromone implementation to another. Moreover, it will be appreciated thatsuch a development effort might be complex and time consuming but wouldnevertheless be a routine undertaking for those of ordinary skill in theart having the benefit of this disclosure. In addition, the compositionused/disclosed herein can also comprise some components other than thosecited. In the summary of the disclosure and this detailed description,each numerical value should be read once as modified by the term “about”(unless already expressly so modified), and then read again as not somodified unless otherwise indicated in context. The term about should beunderstood as any amount or range within 10% of the recited amount orrange (for example, a range from about 1 to about 10 encompasses a rangefrom 0.9 to 11). Also, in the summary and this detailed description, itshould be understood that a concentration range listed or described asbeing useful, suitable, or the like, is intended that any concentrationwithin the range, including the end points, is to be considered ashaving been stated. For example, “a range of from 1 to 10” is to be readas indicating each possible number along the continuum between about 1and about 10. Furthermore, one or more of the data points in the presentexamples may be combined together, or may be combined with one of thedata points in the specification to create a range, and thus includeeach possible value or number within this range. Thus, even if specificdata points within the range, or even no data points within the range,are explicitly identified or refer to a few specific, it is to beunderstood that inventors appreciate and understand that any data pointswithin the range are to be considered to have been specified, and thatinventors possessed knowledge of the entire range and the points withinthe range.

Spacer Fluids Containing Expanding Agents

In an aspect, embodiments relate to compositions comprising water, aviscosifying agent and an expanding agent comprising calcium oxide orcalcined magnesium oxide or both. Such compositions may be spacerfluids.

In a further aspect, embodiments relate to methods comprising preparinga spacer fluid the comprises water, a viscosifying agent and anexpanding agent comprising calcium oxide, calcined magnesium oxide orboth. During a well cementing operation, the spacer fluid is placed inthe well such that the spacer fluid flows between a drilling fluid and acement slurry. The spacer fluid commingles with the drilling fluid orthe cement slurry, thereby forming an interface. The cement slurry andthe interface are cured, wherein the interface expands or does notshrink upon the curing.

The cement slurry may comprise portland cement, pozzolan cement, gypsumcement, high alumina cement, slag cement, lime-silica blends orgeopolymer cements or combinations thereof.

The volume ratio between the cement slurry and the spacer fluid in thecommingled cement slurry and spacer fluid may be between 99:1 and 1:99.

For both aspects, the MgO may be calcined at temperatures between about700° C. and 2000° C., or between 1100° C. and 1300° C.

For both aspects, the viscosifying agent may comprise an organophilicclay, hydrophobically modified silica, hydrophobically modifiedbiopolymers or hydrophobically modified synthetic polymers orcombinations thereof. The hydrophobically modified biopolymer maycomprise acetone-formaldehyde-sodium bisulfate polymer andD-Glucopyranuoic acid, polymer with 6-deoxy-L-mannose, D-glucose andD-mannose, calcium potassium sodium salt. The weight ratio between theacetone-formaldehyde-sodium bisulfate polymer and the D-Glucopyranuoicacid, polymer with 6-deoxy-L-mannose, D-glucose and D-mannose, calciumpotassium sodium salt may be between 80:20 and 20:80, or between66.7:33.3 and 33.3:66.7.

For both aspects, the viscosifying agent may further comprise bentonite,present at a concentration in the viscosifying agent between 0.1 wt %and 10 wt %, or between 0.5 wt % and 5.0 wt %.

For both aspects, the viscosifying agent may be present in thecomposition at a concentration between 0.1 wt % and 10 wt %, or between0.5% and 5.0 wt %.

For both aspects, the expanding agent may be present in the compositionat a concentration between 0.1 wt % and 20 wt %, or between 0.5 wt % and10 wt %. The expanding agent may be a blend of calcium oxide andcalcined magnesium oxide. The weight ratio between the calcium oxide andthe calcined magnesium oxide may vary between 10:90 and 90:10, orbetween 60:40 and 40:60.

For both aspects, the expanding agent may be suspended in a non-aqueousadditive comprising a hydrocarbon liquid, and the expanding agent may bepresent in the non-aqueous additive at a concentration between 10 wt %and 80 wt %, or between 30 wt % and 60 wt %. The hydrocarbon liquid maycomprise alkanes, alkenes, alkynes, cycloalkanes, aromatic hydrocarbons,natural gas liquids, liquid paraffins, naphthas, mineral oils, crudeoils, synthesized hydrocarbon liquids, fuel oils, diesels, gasolines,biomass derived hydrocarbon liquids, coal derived hydrocarbon liquids,or kerosine, or mixtures thereof. The hydrocarbon liquid may be Escaid™110, available from ExxonMobil.

For both aspects, the non-aqueous additive may further comprise adispersant comprising polynaphthalene sulfonate, sulfonated acetoneformaldehyde condensate, polycarboxylate ethers or microparticles orcombinations thereof. The dispersant may be present in the non-aqueousadditive at a concentration between 0.1 wt % and 20 wt %, or between 2.0wt % and 10 wt %.

For both aspects, the non-aqueous additive may further comprise anemulsifier comprising polysorbates or sorbitan esters, or both. Theemulsifier may be present at a concentration between 0.01 wt % and 10 wt%, or 1 wt % to 5 wt %.

For both aspects, the expanding agent may be encapsulated by a coatinghaving a thickness between about 2 μm and 80 μm. The coating maycomprise a polymer comprising a polyester, a polyacrylate, an epoxy, apolyhydroxyacid, a polypeptide, a polyesteramide, a polysulfide, apolysiloxane, a block copolymer comprising blocks joined through esterbonds, or a block copolymer comprising blocks joined through amidebonds, or combinations thereof. Or, the coating may comprise silica thatis sprayed onto the encapsulating agent as a silicate solution.

For both aspects, the compositions may further comprise a weightingagent comprising silica, barite, hematite, calcium carbonate, ilmeniteor manganese tetraoxide or combinations thereof. The density of thecomposition may therefore vary between about 10 lbm/gal (1200 kg/m³) andabout 24 lbm/gal (2880 kg/m³). To achieve lower densities, for exampleas low as 8 lbm/gal (960 kg/m³), the composition may further compriselow-density additives including ceramic microspheres, glass microspheresor plastic beads or combinations thereof. Or, the compositions may befoamed with air or nitrogen.

Non-Aqueous Drilling Fluids Containing Expanding Agents

In a further aspect, embodiments relate to compositions comprising anon-aqueous liquid and an expanding agent comprising calcium oxide orcalcined magnesium oxide or both. The compositions may be drillingfluids.

In a further aspect, embodiments relate to methods comprising preparinga drilling fluid comprising a non-aqueous fluid and an expanding agentcomprising calcium oxide or calcined magnesium oxide or both. During awell cementing operation, the drilling fluid is placed in the well suchthat the drilling fluid flows ahead of a cement slurry. The drillingfluid commingles with the cement slurry, thereby forming an interface.The cement slurry and the interface are cured, wherein the interfaceexpands or does not shrink upon the curing.

A spacer fluid may be placed between the drilling fluid and the cementslurry.

The cement slurry may comprise portland cement, pozzolan cement, gypsumcement, high alumina cement, slag cement, lime-silica blends orgeopolymer cements or combinations thereof.

The volume ratio between the cement slurry and the drilling fluid in thecommingled cement slurry and spacer fluid may be between 99:1 and 1:99.

For both aspects, the non-aqueous fluid may comprise one liquid phase ora water-in-oil emulsion wherein the oil is the external phase.

For both aspects, the MgO may be calcined at temperatures between about700° C. and 2000° C., or between 1100° C. and 1300° C.

For both aspects, the expanding agent may be present in the compositionat a concentration between 0.1 wt % and 20 wt %, or between 0.5 wt % and10 wt %.

For both aspects, the expanding agent may be encapsulated by a coatinghaving a thickness between about 2 μm and 80 μm. The coating maycomprise a polymer comprising a polyester, a polyacrylate, an epoxy, apolyhydroxyacid, a polypeptide, a polyesteramide, a polysulfide, apolysiloxane, a block copolymer comprising blocks joined through esterbonds, or a block copolymer comprising blocks joined through amidebonds, or combinations thereof. Or, the coating may comprise silica thatis sprayed onto the encapsulating agent as a silicate solution.

For both aspects, the expanding agent may be suspended in a non-aqueousadditive comprising a hydrocarbon liquid, and the expanding agent may bepresent in the non-aqueous additive at a concentration between 10 wt %and 80 wt %, or between 30 wt % and 60 wt %. The hydrocarbon liquid maycomprise alkanes, alkenes, alkynes, cycloalkanes, aromatic hydrocarbons,natural gas liquids, liquid paraffins, naphthas, mineral oils, crudeoils, synthesized hydrocarbon liquids, fuel oils, diesels, gasolines,biomass derived hydrocarbon liquids, coal derived hydrocarbon liquids,or kerosine, or mixtures thereof. The hydrocarbon liquid may be Escaid™110, available from ExxonMobil.

For both aspects, the non-aqueous additive may further comprise adispersant comprising polynaphthalene sulfonate, sulfonated acetoneformaldehyde condensate, polycarboxylate ethers or microparticles orcombinations thereof. The dispersant may be present in the non-aqueousadditive at a concentration between 0.1 wt % and 20 wt %, or between 2.0wt % and 10 wt %.

For both aspects, the non-aqueous additive may further comprise anemulsifier comprising polysorbates or sorbitan esters, or both. Theemulsifier may be present at a concentration between 0.01 wt % and 10 wt%, or between 1 wt % and 5 wt %.

For both aspects, the composition may further comprise a weighting agentcomprising silica, barite, hematite, calcium carbonate, ilmenite ormanganese tetraoxide or combinations thereof. The density of thecomposition may therefore vary between about 10 lbm/gal (1200 kg/m³) andabout 24 lbm/gal (2880 kg/m³). To achieve lower densities, for exampleas low as 8 lbm/gal (960 kg/m³), the composition may further compriselow-density additives including ceramic microspheres, glass microspheresor plastic beads or combinations thereof. Or, the compositions may befoamed with air or nitrogen.

For both aspects, the viscosifying agent may comprise an organophilicclay, hydrophobically modified silica, hydrophobically modifiedbiopolymers or hydrophobically modified synthetic polymers orcombinations thereof. The hydrophobically modified biopolymer maycomprise acetone-formaldehyde-sodium bisulfate polymer andD-Glucopyranuoic acid, polymer with 6-deoxy-L-mannose, D-glucose andD-mannose, calcium potassium sodium salt. The weight ratio between theacetone-formaldehyde-sodium bisulfate polymer and the D-Glucopyranuoicacid, polymer with 6-deoxy-L-mannose, D-glucose and D-mannose, calciumpotassium sodium salt may be between 80:20 and 20:80, or between66.7:33.3 and 33.3:66.7.

For both aspects, the viscosifying agent may further comprise bentonite,present at a concentration in the viscosifying agent between 0.1 wt %and 10 wt %, or between 0.5 wt % and 5.0 wt %.

Cement Slurries

In a further aspect, embodiments relate to compositions comprising anaqueous cement slurry and a non-aqueous additive comprising a suspensionof an expanding agent comprising calcium oxide or a mixture of calciumoxide and calcined magnesium oxide.

In a further aspect, embodiments relate to methods comprising preparinga composition comprising an aqueous cement slurry and a non-aqueousadditive comprising a suspension of an expanding agent comprisingcalcium oxide and calcined magnesium oxide or both. During a wellcementing operation, the cement slurry is placed in the well such thatthe cement slurry flows behind a spacer fluid or a drilling fluid orboth. The spacer fluid or the drilling fluid may commingle with thecement slurry, thereby forming an interface. The cement slurry and theinterface are cured, wherein the interface expands or does not shrinkupon the curing.

The aqueous cement slurry may comprise water, portland cement, pozzolancement, gypsum cement, high alumina cement, slag cement, lime-silicablends or geopolymer cements or combinations thereof.

The volume ratio between the cement slurry and the drilling fluid in thecommingled cement slurry and spacer fluid, or between the cement slurryand the spacer fluid in the commingled cement slurry and spacer fluid,may be between 99:1 and 1:99.

For both aspects, the non-aqueous additive may comprise a hydrocarbonliquid. The hydrocarbon liquid may comprise alkanes, alkenes, alkynes,cycloalkanes, aromatic hydrocarbons, natural gas liquids, liquidparaffins, naphthas, mineral oils, crude oils, synthesized hydrocarbonliquids, fuel oils, diesels, gasolines, biomass derived hydrocarbonliquids, coal derived hydrocarbon liquids, or kerosine, or mixturesthereof. The hydrocarbon liquid may be Escaid™ 110, available fromExxonMobil. The hydrocarbon liquid may be present in the non-aqueousadditive at a concentration between 1 wt % and 99 wt %, or between 30 wt% and 70 wt %.

For both aspects, the MgO may be calcined at temperatures between about700° C. and 2000° C., or between 1100° C. and 1300° C.

For both aspects, the expanding agent may be present in the non-aqueousadditive at a concentration between 0.1 wt % and 20 wt %, or between 0.5wt % and 10 wt %.

For both aspects, the non-aqueous additive may further comprise adispersant comprising polynaphthalene sulfonate, sulfonated acetoneformaldehyde condensate, polycarboxylate ethers or microparticles orcombinations thereof. The dispersant may be present in the non-aqueousadditive at a concentration between 0.1 wt % and 20 wt %, or between 2.0wt % and 10 wt %.

For both aspects, the non-aqueous additive may further comprise anemulsifier comprising polysorbates or sorbitan esters, or both. Theemulsifier may be present at a concentration between 0.01 wt % and 10 wt%, or between 1 wt % and 5 wt %.

For both aspects, the composition may further comprise a weighting agentcomprising silica, barite, hematite, calcium carbonate, ilmenite ormanganese tetraoxide or combinations thereof. The density of thecomposition may therefore vary between about 10 lbm/gal (1200 kg/m³) andabout 24 lbm/gal (2880 kg/m³). To achieve lower densities, for exampleas low as 8 lbm/gal (960 kg/m³), the composition may further compriselow-density additives including ceramic microspheres, glass microspheresor plastic beads or combinations thereof. Or, the compositions may befoamed with air or nitrogen.

EXAMPLES

The following examples are presented to provide a general illustrationof the present disclosure, and are not intended to limit the scope ofthe disclosure in any way.

The following examples describe expansion experiments that wereperformed using five fluid formulations, described below.

Formulation 1 was a 15.8 lbm/gal (1900 kg/m³) Class G cement slurry,with 0.1 gal/94-lb sack (0.88 L/tonne of cement) silicone antifoam agentand 0.28 gal/sk (24.86 L/tonne of cement) liquid expansion additive. Theliquid expansion additive had a 50:50 solid:liquid ratio. The solidportion was CaO and calcined MgO in a 60:40 weight ratio. The liquidphase was 97% Escaid™ 110 oil and 3% viscosifying polymer. Theviscosifying polymer was poly(propylene-alt-ethylene) multi-arm,available from Kraton Corporation, Houston, Tex., USA.

Formulation 2 was a 14.0-lbm/gal (1680 kg/m³) aqueous spacer fluidcontaining an expansion additive. The fluid contained 0.1 gal/bblsilicone antifoam, 4 lbm/bbl bentonite, 4 lbm/bbl of a viscosifiercomprising 66.7% acetone-formaldehyde-sodium bisulfate polymer and 33.3%D-Glucopyranuoic acid, polymer with 6-deoxy-L-mannose, D-glucose andD-mannose, calcium potassium sodium salt, 5.3 gal/bbl liquid expansionadditive (as described in Formulation 1) and 6.8 lbm/bbl bariteweighting agent.

Formulation 3 was a 14.0-lbm/gal (1680 kg/m³) aqueous spacer fluidwithout an expansion additive. The fluid contained 0.1 gal/bbl siliconeantifoam, 4 lbm/bbl bentonite, 4 lbm/bbl of a viscosifier comprising66.7% acetone-formaldehyde-sodium bisulfate polymer and 33.3%D-Glucopyranuoic acid, polymer with 6-deoxy-L-mannose, D-glucose andD-mannose, calcium potassium sodium salt and 6.8 lbm/bbl bariteweighting agent.

Formulation 4 was a 10.8 lbm/gal (1300 kg/m³) oil-base drilling fluidcontaining an expansion additive. The fluid composition is given inTable 1 below.

TABLE 1 Formulation 4 composition. Concentration Field, lbm per bbl Lab,g for 350 ml # Products of prepared fluid prepared fluid  1 MG-3 baseoil, 165.21 165.21 available from Petronas  2 Calcium chloride 24.7324.73  3 VG SUPREME 6.00 6.00 organophilic clay viscosifier, availablefrom Schlumberger  4 Calcium hydroxide 5.00 5.00  5 VERSATROL M 5.005.00 asphaltic resin, available from Schlumberger  6 Calcium carbonate10.00 10.00  7 VERSAMOD gelling 1.00 1.00 agent, available fromSchlumberger  8 SUREMUL PLUS 6.00 6.00 emulsifier, available fromSchlumberger  9 Water 82.07 82.07 10 Barite 148.58 148.58 11 60:40 blendof CaO 29.86 29.86 and calcined MgO

Formulation 5 was a 10.8 lbm/gal (1300 kg/m³) oil-base drilling fluidwithout an expansion additive. The fluid composition is given in Table 2below.

TABLE 2 Formulation 5 composition. Concentration Field, lbm per bbl Lab,g for 350 ml # Products of prepared fluid prepared fluid  1 MG-3 baseoil, 165.21 165.21 available from Petronas  2 Calcium chloride 24.7324.73  3 VG SUPREME 6.00 6.00 organophilic clay viscosifier, availablefrom Schlumberger  4 Calcium hydroxide 5.00 5.00  5 VERSATROL M 5.005.00 asphaltic resin, available from Schlumberger  6 Calcium carbonate10.00 10.00  7 VERSAMOD gelling 1.00 1.00 agent, available fromSchlumberger  8 SUREMUL PLUS 6.00 6.00 emulsifier, available fromSchlumberger  9 Water 82.07 82.07 10 Barite 148.58 148.58

Linear expansion tests were performed with the above formulations. Thefluids were prepared and mixed in a 200-mL beaker of either pure fluidor with fluid blends to simulate commingling in a wellbore duringplacement. The test fluids were placed within an expansion cell (FIG. 1) and then lowered into a water bath. Expansion measurements were takenperiodically during curing in the water bath. Additional informationconcerning the expansion test method may be found in the followingpublication. Dargaud B and Boukhelifa L: “Laboratory Testing, Evaluationand Analysis of Well Cements,” in Nelson E B and Guillot D (eds.): WellCementing—2^(nd) Edition, Schlumberger (2006) 641-643.

Example 1

Testing was conducted to determine the effects of commingling between acement slurry containing an expanding agent and oil-base drilling fluidswith and without an expanding agent. Three fluids were tested: a controlsystem of Formulation 1 alone; an 80:20 volume ratio of Formulation 1and Formulation 4; and an 80:20 volume ratio of Formulation 1 andFormulation 5. The curing temperature was 54° C. The results, shown inFIG. 2 , reveal that the best performing system was the one in which thecement slurry was contaminated with the oil-base drilling fluidcontaining the expansion agent. Next, was Formulation 1 alone. Thesmallest expansion was observed when the oil-base drilling fluid did notalso contain the expansion agent. Thus, commingling of the cement slurrywith oil-base drilling fluid containing expansion agent leads to betterexpansion and bonding between the set cement and the casing andformation surfaces, leading to better zonal isolation.

Example 2

Testing was conducted to determine the effects of commingling between acement slurry containing an expanding agent and aqueous spacer fluidswith and without an expanding agent. Three fluids were tested: a controlsystem of Formulation 1 alone; an 80:20 volume ratio of Formulation 1and Formulation 2; and an 80:20 volume ratio of Formulation 1 andFormulation 3. The curing temperature was 54° C. The results, shown inFIG. 3 , reveal that the best performing system was the one in which thecement slurry was contaminated with the spacer fluid containing theexpansion agent. This was followed by Formulation 1 alone. The smallestexpansion was observed when the spacer fluid did not also contain theexpansion agent. Thus, commingling of the cement slurry with spacerfluid containing expansion agent leads to better expansion and bondingbetween the set cement and the casing and formation surfaces, leading tobetter zonal isolation.

The preceding description has been presented with reference to presentembodiments. Persons skilled in the art and technology to which thisdisclosure pertains will appreciate that alterations and changes in thedescribed structures and methods of operation can be practiced withoutmeaningfully departing from the principle, and scope of this presentdisclosure. Accordingly, the foregoing description should not be read aspertaining only to the precise structures described and shown in theaccompanying drawings, but rather should be read as consistent with andas support for the following claims, which are to have their fullest andfairest scope.

1. A composition, comprising: an aqueous cement slurry; and anon-aqueous additive comprising a suspension of an expanding agentcomprising calcium oxide or a mixture of calcium oxide and calcinedmagnesium oxide.
 2. The composition of claim 1, wherein the non-aqueousadditive further comprises a hydrocarbon liquid; wherein the hydrocarbonliquid is present in the non-aqueous additive at a concentration between1 wt % and 99 wt %.
 3. The composition of claim 2, wherein thehydrocarbon liquid comprises alkanes, alkenes, alkynes, cycloalkanes,aromatic hydrocarbons, natural gas liquids, liquid paraffins, naphthas,mineral oils, crude oils, synthesized hydrocarbon liquids, fuel oils,diesels, gasolines, biomass derived hydrocarbon liquids, coal derivedhydrocarbon liquids, or kerosene, or mixtures thereof.
 4. Thecomposition of claim 1, wherein the aqueous cement slurry compriseswater, portland cement, pozzolan cement, gypsum cement, high aluminacement, slag cement, lime-silica blends or geopolymer cements orcombinations thereof.
 5. The composition of claim 1, wherein thecalcined magnesium oxide is calcined at a temperature between 700° C.and 2000° C.
 6. The composition of claim 1, wherein the expanding agentis present in the non-aqueous additive at a concentration between 10 wt% and 80 wt %.
 7. The composition of claim 1, wherein the non-aqueousadditive further comprises a dispersant comprising polynaphthalenesulfonate, sulfonated acetone formaldehyde condensate, polycarboxylateethers, or micro particles or combinations thereof; wherein thedispersant is present in the non-aqueous additive at a concentrationbetween 0.1% and 20 wt %.
 8. The composition of claim 1, wherein thenon-aqueous additive further comprises an emulsifier comprisingpolysorbates or sorbitan esters, or both; wherein the emulsifier ispresent in the non-aqueous additive at a concentration between 0.01 wt %and 10 wt %.
 9. The composition of claim 1, further comprising aweighting agent, the weighting agent comprising silica, barite,hematite, ilmenite or manganese tetraoxide or combinations thereof. 10.A method, comprising: (a) preparing a composition comprising an aqueouscement slurry and a non-aqueous additive comprising a suspension of anexpanding agent comprising calcium oxide and calcined magnesium oxide orboth; (b) during a well cementing operation, placing the cement slurryin the well such that the cement slurry flows behind a spacer fluid or adrilling fluid, or both. (c) causing the spacer fluid or the drillingfluid to commingle with the cement slurry, thereby forming an interface;and (d) curing the cement slurry and the interface, wherein theinterface expands or does not shrink upon the curing.
 11. The method ofclaim 10, wherein the aqueous cement slurry comprises water, portlandcement, pozzolan cement, gypsum cement, high alumina cement, slagcement, lime-silica blends or geopolymer cements or combinationsthereof.
 12. The method of claim 10, wherein a volume ratio between thecement slurry and the spacer fluid in the commingled cement slurry andspacer fluid, or a volume ratio between the cement slurry and thedrilling fluid, is between 99:1 and 1:99.
 13. The method of claim 10,wherein the non-aqueous additive further comprises a hydrocarbon liquid.14. The method of claim 13, wherein the hydrocarbon liquid comprisesalkanes, alkenes, alkynes, cycloalkanes, aromatic hydrocarbons, naturalgas liquids, liquid paraffins, naphthas, mineral oils, crude oils,synthesized hydrocarbon liquids, fuel oils, diesels, gasolines, biomassderived hydrocarbon liquids, coal derived hydrocarbon liquids, orkerosene, or mixtures thereof; wherein the hydrocarbon liquid is presentin the non-aqueous additive at a concentration between 1 wt % and 99 wt%.
 15. The method of claim 10, wherein the calcined magnesium oxide iscalcined at a temperature between 700° C. and 2000° C.
 16. The method ofclaim 10, wherein the expanding agent is present in the non-aqueousadditive at a concentration between 10 wt % and 80 wt %.
 17. The methodof claim 10, wherein the non-aqueous additive further comprises adispersant comprising polynaphthalene sulfonate, sulfonated acetoneformaldehyde condensate, polycarboxylate ethers, or micro particles orcombinations thereof; wherein the dispersant is present in thenon-aqueous additive at a concentration between 0.1 wt % and 20 wt %.18. The method of claim 10, wherein the non-aqueous additive furthercomprises an emulsifier comprising polysorbates or sorbitan esters, orboth; wherein the emulsifier is present in the non-aqueous additive at aconcentration between 0.01 wt % and 10 wt %.
 19. The method of claim 10,wherein the cement slurry further comprises a weighting agent, theweighting agent comprising silica, barite, hematite, ilmenite ormanganese tetraoxide or combinations thereof.